Eclipse Combustion Engineering Guide - Burnerparts
Eclipse Combustion Engineering Guide - Burnerparts
Eclipse Combustion Engineering Guide - Burnerparts
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LIQUID HEATING – BURNER SIZING GUIDELINES<br />
I. Tank Heating<br />
To determine the immersion burner size for heating a<br />
liquid tank, conduct two heat balances–one for heatup<br />
requirements, the other for steady-state operating<br />
requirements. Use the larger of the two Btu inputs<br />
obtained from these calculations.<br />
A. Heat Balance – Heatup Requirements<br />
1.Heat to water<br />
Btu/hr = Lb water x temperature rise, °F<br />
heatup time required, hr<br />
or<br />
Btu/hr = 8.3 x gallons water x temperature rise, °F<br />
heatup time required, hr<br />
or<br />
Btu/hr = 62.4 x cu ft water x temperature rise, °F<br />
heatup time required, hr<br />
Common practice allows the following heatup<br />
times for various size tanks:<br />
Tank Capacity Heatup<br />
Gallons Cu Ft Time, hr<br />
0-375 0-50 2<br />
375-750 50-100 4<br />
750-1500 100-200 6<br />
Over 1500 Over 200 8<br />
2.Surface losses – evaporation & radiation<br />
Btu/hr = Exposed bath surface x heat loss<br />
from Table 1.<br />
3.Tank wall losses<br />
Btu/hr = Total sq ft of tank walls & bottom x wall<br />
loss from Table 1.<br />
4.Tank heat storage<br />
Btu/hr =<br />
Total sq ft, tank walls & bottom x storage, Table 1.<br />
heatup time required, hr<br />
5.Total heatup requirements<br />
Heat to water<br />
+ Surface losses<br />
+ Tank wall losses<br />
+ Tank heat storage<br />
= Total heatup requirement<br />
47<br />
B. Heat Balance – Steady State Heat Requirements<br />
1.Heat to workload<br />
Btu/hr =<br />
Lb of work processed x<br />
hr<br />
specific heat x temperature rise, °F<br />
(Work weight must include all baskets & fixtures)<br />
Specific heat of steel is 0.14 Btu/lb - °F.<br />
See pages 37 to 39 for other materials.<br />
2.Surface losses – evaporation & radiation<br />
Same as Step A.2.<br />
3.Tank wall losses<br />
Same as Step A.3.<br />
4.Heat to makeup water<br />
Btu/hr =<br />
makeup rate, gal/hr x 8.3 x temperature rise, °F<br />
5.Total steady state heat requirement<br />
Heat to workload<br />
+ Surface losses<br />
+ Tank wall losses<br />
+ Heat to makeup water<br />
= Total steady state requirement<br />
C. Compare the heat requirements calculated in<br />
Steps A.5 and B.5. Select the larger of the two .<br />
(This is the net hourly input to the tank.)<br />
D. Gross Heat Input (Burner Firing Rate)<br />
Gross Input, Btu/hr = Net Input from A.5 or B.5 x 100<br />
% Efficiency required<br />
Efficiency is a function of immersion tube<br />
length and burner firing rate. 70% is a commonly<br />
used efficiency rating.<br />
E. Immersion Tube Sizing<br />
See burner manufacturer’s product literature<br />
for tube sizing recommendations.<br />
Table 1. Tank losses & storage<br />
Surface Losses, Wall Losses, Btu/sq ft-hr Heat Storage,<br />
Liquid Btu/sq ft-hr Btu/sq ft<br />
Temperature, Evapor- Radia- Insulation Thickness Steel Thickness<br />
°F ation* tion Total* None 1" 2" 3" 1/8" 1/4"<br />
90 80 50 130 50 12 6 4 21 42<br />
100 160 70 230 70 15 8 6 28 56<br />
110 240 90 330 90 19 10 7 35 70<br />
120 360 110 470 110 23 12 9 42 84<br />
130 480 135 615 135 27 14 10 49 98<br />
140 660 160 820 160 31 16 12 56 112<br />
150 860 180 1040 180 34 18 13 63 126<br />
160 1100 210 1310 210 38 21 15 70 140<br />
170 1380 235 1615 235 42 23 16 77 154<br />
180 1740 260 2000 260 46 25 17 84 168<br />
190 2160 290 2450 290 50 27 19 91 182<br />
200 2680 320 3000 320 53 29 20 98 196<br />
210 3240 360 3590 360 57 31 22 105 210<br />
220 4000 420 4420 380 62 33 23 112 224<br />
250 — 510 — 510 70 40 25 133 266<br />
275 — 600 — 600 81 45 29 151 301<br />
300 — 705 — 705 92 51 33 168 336<br />
325 — 850 — 850 103 57 36 186 371<br />
350 — 990 — 990 114 63 40 203 406<br />
400 — 1335 — 1335 138 75 49 238 476<br />
*Water or water-based solutions only.